| dc.contributor.author | Özmen, Dilek | |
| dc.contributor.author | Özmen, Atilla | |
| dc.date.accessioned | 2019-06-28T11:11:37Z | |
| dc.date.available | 2019-06-28T11:11:37Z | |
| dc.date.issued | 2006 | |
| dc.identifier.isbn | 8086059456 | |
| dc.identifier.isbn | 9788086059457 | |
| dc.identifier.uri | https://hdl.handle.net/20.500.12469/1648 | |
| dc.description.abstract | (Liquid + liquid) equilibrium (LLE) data for (water + propionic acid + solvent) were measured at T= 298.2 K and atmospheric pressure. The solvents were methyl isoamyl ketone (5-methyl-2-hexanone) and diisobutyl ketone. The tie-line data were predicted by the UNIFAC method. A comparison of the extracting capabilities of the solvents was made with respect to distribution coefficients separation factors and solvent free selectivity bases. | en_US] |
| dc.language.iso | eng | en_US |
| dc.rights | info:eu-repo/semantics/closedAccess | en_US |
| dc.subject | Diisobutyl ketone | en_US |
| dc.subject | Liquid-liquid equilibria | en_US |
| dc.subject | Methyl isoamyl ketone | en_US |
| dc.subject | Propionic acid | en_US |
| dc.title | Liquid-liquid equilibria of water+propionic acid+solvent ternaries at 298.2 K | en_US |
| dc.type | conferenceObject | en_US |
| dc.relation.journal | CHISA 2006 - 17th International Congress of Chemical and Process Engineering | en_US |
| dc.department | Fakülteler, Mühendislik ve Doğa Bilimleri Fakültesi, Elektrik-Elektronik Mühendisliği Bölümü | en_US |
| dc.identifier.scopus | 2-s2.0-34748854908 | en_US |
| dc.institutionauthor | Özmen, Atilla | en_US |
| dc.relation.publicationcategory | Konferans Öğesi - Uluslararası - Kurum Öğretim Elemanı | en_US |
